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Publication numberUS3522692 A
Publication typeGrant
Publication dateAug 4, 1970
Filing dateJan 23, 1968
Priority dateJan 23, 1968
Publication numberUS 3522692 A, US 3522692A, US-A-3522692, US3522692 A, US3522692A
InventorsBeach Gerald H, Brookman Roger S
Original AssigneeDustex Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Gas scrubber
US 3522692 A
Abstract  available in
Images(2)
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Claims  available in
Description  (OCR text may contain errors)

R. S. BROOKMAN ET AL GAS SCRUBBER 2 Sheets-Sheet l Filed Jan. 25, 1968 INVENTORS. f Fqyea' Brooman arm'efaldieac' BY M HSM/V ATTORNEYS.

AU@ 4;"1970 n. s. BRooKMAN Erm. 3,522,692

GAs scnuna Filed Jan. 23. 1968 2 Sheets-Sheet 2 Bwqleww ATToRNEYs.

3,522,692 GAS SCRUBBER Roger S. Broekman, East Aurora, and Gerald H. Beach, Williamsville, N.Y., assignors to 'Dustex Corp., Buffalo, N.Y., a corporation of New York Filed Jan. 23, 1968, Ser. No. 699,914 Int. Cl. B01d 47/00 U.S. Cl. 55-233 6 Claims ABSTRACT F THE DISCLOSURE A contaminated gas stream is directed through a scrubber and then through spaced apart primary and secondary fil-ters composed of a reticulated polyurethane foam. The primary filter is wetted, and a fine spray Wets the gas stream passing from the primary filter to the secondary filter.

BACKGROUND OF THE INVENTION This invention relates to the gas scrubbing art, and more specifically to a new and useful wet collector capable of removing condensible odorous vapors as well as particulate contaminants.

The cleaning of vaporous eiuents, thereby to avoid contamination of the earths atmosphere, is a matter of increasing concern. Various efforts have been made andY continue to be made to provide eicient scrubbers for the various types of gaseous discharges normally encountered. Howeven in many situations these efforts have met with limited success, at best, and this is particularly so in the removal of contaminants normally discharged as vapors.

For example, the gaseous eiuent from coffee roasting processes poses a severe problem because of the variety and type of contaminants contained therein including, in addition to chaff and other solid particulate material, aldehydes, fats, oils, waxes and organic acids many of which are discharged in the vaporous state and which often produce noxious odors.

So far as we are aware, conventional scrubbers have not worked satisfactorily under such conditions, and it has been necessary to resort to after-burning and other arrangements the cost of which often exceeds the cost of the roasting process itself.

SUMMARY OF THE INVENTION This invention provides a scrubber utilizing what is believed to be a unique combination of filters and wetting sprays.

A primary object of this invention is to provide a wet scrubber capable of removing both condensible vapors and solid particulates from a contaminated gas stream.

YAnother object of -this invention is to accomplish the foregoing in an arrangement consuming a relatively smalll quantity of liquid.

Still another object of this invention is to provide the foregoing in highly efficient arrangement, capable of handling large volumes of contaminated gas at elevated temperatures.

The foregoing and other objects, advantages and characterizing features of our invention will becomeclearly apparent from the ensuing detailed description of an illustrative embodiment thereof, reference being made to the accompanying drawings wherein like reference numerals denote like parts throughout the Various views.

DESCRIPTION OF THE DRAWING FIGURES FIG. 1 is a generally schematic layout of a scrubber installation of this invention; and

United States Patent 3,522,692 Patented Aug. 4, 1970 ICC FIG. 2 is a generally schematic layout of the liquid circuit thereof.

DETAILED DESCRIPTION OF THE ILLUSTRATED EMBODIMENT Referring now in detail to the accompanying drawings, there is shown a scrubber of our invention, generally designated 1, communicating via conduit 2, chaff cyclone 3 and conduit 4 with a roaster 5. While the instant disclosure is directed to a coffee roaster scrubber installation, it will be appreciated that our invention is not limited thereto. Cyclone 3 and roaster 5 can be of any desired construction and are not part, per se, of our invention whereby a detailed description thereof is unnecessary.

Scrubber 1 includes a housing 7 of any suitable configuration, having an inlet 8 adjacent its lower end, above a liquid reservoir 9. An extension 10 of conduit 2 extends from inlet 8 to a downwardly directed inlet conduit portion 11 of enlarged cross section, turned at 90 to inlet conduit 10 and having its open, lower end submerged in the liquid contained in reservoir 9. An exhaust fan 12 communicates via conduit 13 With the clean air outlet 14 from scrubber 1, being regulated by means including a damper 15 having an actuator 16 connected to a draft controller 17 which has a pressure responsive connection at 18 with the roaster discharge conduit 4. In this way, the action of exhaust fan 12 is responsive to the discharge'pressure from roaster 5 in a manner understood by those skilled in the art, it being understood that actuator 16, controller 17 and their connections are conventional.

Our invention is particularly concerned with scrubber 1 which, in addition to the downturn inlet 11 and liquid reservoir 9, includes a primary filter 20 and a secondary filter 21. In the illustrated embodiment, primary filter 20 extends across scrubber 1 above reservoir 9, and secondary filter 21 is above filter 20 in generally parallel relation thereto. However, other orientations of filters 20 and 21 are possible.

A liquid drain connection 22 extends from the bottom of reservoir 9, and has a connection 23 to a circulating pump system generally designated 24 in FIG. 1 and shown in detail in FIG. 2.

Referring now to FIG. 2, pump system 24 is seen to include a circulating pump 25 having an inlet via conduit 23 and a vent into housing 1 immediately above reservoir 9 via conduit 26. A manual fill conduit 27 also can be provided.

The discharge from pump 25 is transmitted via conduit 28 and solenoid controlled valve 29 to a filter 30 of any conventional configuration, preferably of the straight through type, having a releasable coupling to conduits 28 and 31. From filter 30r liquid is passed via conduit 31 and another solenoid control valve 32 to a splash nozzle 33 directed downwardly toward primary filter 20 and discharging the liquid in a coarse, heavy spray so as to thoroughly wet filter 20 completely throughout, notwithstanding the oppositely moving gas stream.

A series of fine spray nozzles 35 receive liquid via conduit 36 and a filter 37. While conduit 36 can be connected to conduit 31 for receiving recirculated liquid it is preferred that nozzles 35 be provided with clean, makeup liquid from any suitable source, not shown. Nozzles 35 produce a fog-like spray, such that they thoroughly wet the gas stream passing from primary filter 20 to secondary filter 21 with a spray or mist which is carried along by the moving gas stream to secondary filter 21.

Drain valves 38 and 39 are provided, the latter being in a by-pass drain conduit 40' leading from a conduit 41 controlled by a solenoid control valve 42 to a return conduit 43 connected to drain 22. An atmospheric level control 44 is connected to reservoir 9 via conduit 45 for maintaining the liquid in reservoir 9 at a predetermined level.

A gas bladder accumulator 46 is connected to conduit 31, and has connected thereto a pressure switch 47 and timer 48. Upon a predetermined pressure drop across filter 30, switch 47 causes normally open valves 29 and 32 to close, and normally closed valve 42 to open, for cleaning filter 30. After a filter cleaning cycle of predetermined time, timer 48 restores valves 29, 32 and 42 to their normal position, for normal operation.

The down turned inlet section 11 provides an impingement section, causing heavier particles to separate and drop into the reservoir 9 from which they are drained and subsequently removed. The gas stream agitates the liquid in reservoir 9, in which the inlet 11 is immersed, producing a high degree of turbulence for agglomerating and scrubbing of the gas stream as it exits around the edge of inlet 11. The liquid in reservoir 9 also cools the gas stream, to begin condensing of the vaporous contaminants therein.

It will be appreciated that other forms of scrubber of the wet collector type can be used in place of inlet section 11 and reservoir 9.

It is a particular feature of our invention that primary filter and secondary filter 21 comprise, in each case, reticulated polyurethane foam material. Such foams are commercially available from Scott Paper Company, Philadelphia, Pa., under the trademark Scottfoam and are fully disclosed and described, together with processes for their production in U.S. Pat. 3,171,820 issued to said Scott Paper Company under date of Mar. 2, 1965 on an application filed in the name of Robert A. Volz. Since these foams are commercially available, and per se no part of our invention, a detailed disclosure thereof herein appears to be unnecessary. Suf-lice it to say that we use reticulated polyurethane foams such as are disclosed in said patent, each filter 20, 21 comprising a slab thereof.

The reticulated products of the present invention can be characterized as a polyurethane resin structure in which the strands forming the S-dimensional network intersect in an integrally formed non-planar nexus, and define, in skeletal form, the outline of multi-sided polyhedral cells. The average diameter of the polygonal cell faces outlined by the strands may vary, as determined by the pore size or cell face diameter of the cellular structures from which the skeletal structures are obtained, from about 0.05 mm. to about 20 mm.

It is important that the foam not be glazed and smooth, but that the strands have tendrils and various strand nexuses have ravel ends making the cellular network somewhat hairy in appearance. This aids significantly in the collecting action of filters 20 and 21.

Further in accordance with our invention, primary lter 20 is a foam of relatively large cell size, while secondary filter 21 is a foam of relatively small cell size. The larger cell size of primary filter 20 lengthens the service time of the filter by decreasing the rate at which the face of the filter plugs with contaminants.

Primary lter 20 is maintained continually-wetted, throughout, by splash nozzle 33, and promotes liquid-gas contact. As a result, the temperature of the gas stream is lowered, condensing some of the contaminating vapor, some of which collects on the filter. Also, certain of the contaminating gases, such as the aldehydes, are absorbed in the liquid and thereby removed.

As the partially cooled gas stream passes from primary filter 20 to secondary filter 21 it is wetted again by the line spray from nozzles 35. These produce a fog-like atmosphere, to provide maximum total contact area between the liquid discharged from nozzles 35 and the gas stream. This results in added cooling and condensing, to-

gether with agglomeration between the fine liquid droplets and the condensed contaminants including those which passed through the primary filter 20.

Secondary filter 21 is moistened by the fog or mist, which is carried by the gas stream into the secondary filter, and therefore promotes liquid-gas Contact for additional removal of contaminants through collection and absorption. Also, filter 21 eliminates the moisture from the gas stream, whereby the gas discharging from secondary filter 21 is dry.

The scrubber of this invention has proven highly effective in handling condensible odorous vapors, such that no odor is detectable in the gas stream exiting from the scrubber. The liquid reservoir, together with the thoroughly wetted filter 20 and the fog spray 35 reduce the temperature of the gas stream to a level causing these contaminants to condense and collect on the filters, through both impingement and contact. The relatively large cell filter 20 is cleaned, to some degree, by the water from nozzle 33, and the arrangement is such that a significantly long filter life is provided both filters. The scrubber can handle substantial variations in both volume and temperature of the gas, as during the quench part of a roasting cycle, and is capable of effectively trapping and removing the myriad contaminants of the gas stream even where the latter initially is at an elevated temperature. Obviously, the scrubber of our invention is useful in a wide variety of situations.

Accordingly, it is seen that our invention fully accomplishes its intended objects. While a single embodiment has been disclosed, that has been done by way of illustration without thought of limitation, it being understood that variations and modifications will readily occur to those skilled in the art and are intended to be included in the appended claims.

What is claimed is:

1. Apparatus for separating contaminants from a gas stream comprising a housing having a contaminated gas inlet and a clean gas outlet, a primary filter in and across said housing downstream of said inlet, a secondary filter in and across said housing downstream of said primary filter, means for moving a gas stream from said inlet through said primary and secondary filters to said outlet, each of said filters comprising a reticulated polyurethane foam, first liquid discharge means directed toward said primary filter and operable to maintain the same continually wetted substantially throughout, and second liquid discharge means comprising fine spray means between said filters producing a fog-like mist carried along by the moving gas stream and wetting the gas stream passing from said primary filter to said secondary filter, said secondary filter also comprising a moisture eliminator, said filters being superposed above said inlet, said first liquid discharge means comprising coarse spray means also positioned between said Ifilters and discharging liquid in a heavy spray onto said primary filter against the moving gas stream.

2. Apparatus as set forth in claim 1, wherein said primary filter comprises a foam of relatively large cell size, and said secondary filter comprises a foam of relatively small cell size.

3. Apparatus as set forth in claim 1, together with gas scrubber means between said inlet and said primary filter providing additional gas-liquid contact and particle removal.

4. Apparatus as set forth in claim 3, said gas scrubber means comprising a liquid reservoir, said filters being superposed above said reservoir, and said inlet including a downwardly directed conduit portion having an open lower end submerged in the liquid contained in said reservoir.

5. Apparatus as set forth in claim 1, wherein said fine spray means are positioned between said primary filter and said coarse spray means.

6. Apparatus as set forth in claim 1, said foam comprising strands having tendrils and strand nexuses having ravel ends.

References Cited UNITED STATES PATENTS Diehl 55-96 Somers 55-333 Walter 55-228 Horvath 55-333 McKamy 55-223 McIlvaine et al. 55-233 Lichtenfels 55-85 Pabst et al. 55-227 Hunn 55-522 Volz 261-94 Weatherston et al. 261-96 Vosseller 55-90 De Bellis 55-223 Plizak et a1. 55-485 Robjohns 261-94 Wisting 55-228 Rogers 55-228 McKeown 55-233 Gaggnaire 261-98 Sackett 55-233 10 FRANK W. LUTTER, Primary Examiner B. NOZICK, Assistant Examinerv U.S. Cl. X.R.

Patent Citations
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Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3861889 *Dec 26, 1973Jan 21, 1975Mitsui Toatsu ChemicalsProcess for removing dust from a gas stream
US3885929 *Oct 26, 1973May 27, 1975United Mcgill CorpMethod and apparatus for cleaning exhaust gas
US3961018 *Dec 6, 1973Jun 1, 1976United Air Specialists, Inc.Reaction with methylamine and dimethylamine in vapor phase
US4028527 *Dec 2, 1974Jun 7, 1977Thagard Jr George FApparatus and control system for heating asphalt
US4135908 *Jul 20, 1977Jan 23, 1979Peter WidmerMethod of and apparatus for aerobic decomposition of organic solids
US4155977 *Aug 11, 1977May 22, 1979Baker Bob GPollution control system
US4226179 *Nov 15, 1978Oct 7, 1980Kenneth T. PlaceApparatus for applying sprout inhibitor
US4460552 *May 26, 1981Jul 17, 1984Steuler Industriewerke, G.M.B.H.Process for the separation of air components, such as difficultly absorbable air impurities, out of air-gas mixtures
US6132493 *Aug 5, 1998Oct 17, 2000Church; C. DanielApparatus and method for washing air with a liquid without an eliminator
US7285300 *Nov 6, 1998Oct 23, 2007Group 32 Development & Engineering, Inc.Process of roasting coffee beans in which the darkness and/or color of the beans is monitored to ensure proper roasting
US7998515 *Jun 6, 2007Aug 16, 2011Group 32 Development And Engineering, Inc.Method and apparatus for preventing the discharge of powdery caffeine during coffee roasting
WO1998005653A1 *Jul 31, 1996Feb 12, 1998Bayer AgProcess for preparing substituted 4,4'-diaminostilbene-2,2'-disulphonic acid salts
Classifications
U.S. Classification96/276, 96/342, 55/283, 55/342, 96/361, 55/522, 261/36.1, 55/467, 261/98, 96/298, 261/122.1, 261/3, 55/482
International ClassificationB01D47/06
Cooperative ClassificationB01D47/06
European ClassificationB01D47/06